Recovery of valuable metals from manganese purification sludge (SPS) containing Mn-Ni-Co sulfide and preparation of battery-grade Ni-Co-Mn sulfate solution

IF 4.8 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING
Leiting Yue , Mingyu Wang , Jia Li , Wenjuan Guan , Qinggang Li , Zuoying Cao , Shengxi Wu , Guiqing Zhang
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Abstract

The manganese production industry produces a large amount of sulfide purification sludge (SPS) every year, representing a hazardous solid waste but also a valuable secondary resource for Ni, Co, and Mn. In this paper, the recovery of Ni, Co, and Mn from the SPS was achieved by (i) leaching with a solution of hydrogen peroxide, (ii) selectively extracting nickel, cobalt and manganese, (iii) solvent extraction for zinc removal, and finally obtained the battery-grade Ni-Co-Mn sulfate solution. During the hydrogen peroxide solution leaching stage, the leaching efficiency of Co, Mn, and Ni reached 98.5%, 98.6%, and 95.6%, respectively. A synergistic extraction system (SES) consisting of decyl 4-picolinate and dinonylnaphthalene sulfonic acid was used to selectively extract Ni, Co, and part of Mn, and the extraction of Ni and Co was >99.8% and 95.5%, respectively. The loaded organic was subjected to four-stage countercurrent scrubbing using a 5 g/L H2SO4 solution, resulting in nearly 100% removal of Ca and Mg. After that, 150 g/L H2SO4 was used to strip Ni, Co, and Mn from the loaded organic to obtain a crude Ni-Co-Mn sulfate solution. Finally, D2EHPA was utilized for the extraction of impurity Zn from the stripping solution to obtain a battery-grade Ni-Co-Mn sulfate solution with <5 × 10−4 g/L of Zn. Compared to traditional technology, the novel process not only enables the recovery of valuable Ni, Co, and Mn in SPS but also facilitates their direct preparation into battery-grade nickel‑cobalt‑manganese sulfate solution, which has the advantages of a short process and high added value.

从含硫化锰-镍-钴的锰净化污泥(SPS)中回收有价金属并制备电池级硫酸镍-钴-锰溶液
锰生产行业每年都会产生大量的硫化净化污泥(SPS),这是一种危险的固体废物,但同时也是一种宝贵的镍、钴和锰的二次资源。本文通过以下方法从硫化净化污泥中回收镍、钴和锰:(1) 过氧化氢溶液浸出;(2) 选择性提取镍、钴和锰;(3) 溶剂萃取除锌,最终获得电池级硫酸镍钴锰溶液。在过氧化氢溶液浸出阶段,钴、锰和镍的浸出效率分别达到 98.5%、98.6% 和 95.6%。由 4-吡啶甲酸癸酯和二壬基萘磺酸组成的协同萃取系统(SES)可选择性地萃取镍、钴和部分锰,镍和钴的萃取率分别为 99.8%和 95.5%。使用 5 g/L H2SO4 溶液对负载有机物进行四级逆流洗涤,结果 Ca 和 Mg 的去除率接近 100%。然后,用 150 g/L H2SO4 从负载有机物中剥离出镍、钴和锰,得到粗硫酸镍钴锰溶液。最后,利用 D2EHPA 从剥离液中提取杂质 Zn,得到电池级硫酸镍-钴-锰溶液,其中 Zn 含量为 5 × 10-4 g/L。与传统工艺相比,该新型工艺不仅能回收 SPS 中有价值的镍、钴和锰,还能将它们直接制备成电池级硫酸镍钴锰溶液,具有工艺流程短、附加值高等优点。
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来源期刊
Hydrometallurgy
Hydrometallurgy 工程技术-冶金工程
CiteScore
9.50
自引率
6.40%
发文量
144
审稿时长
3.4 months
期刊介绍: Hydrometallurgy aims to compile studies on novel processes, process design, chemistry, modelling, control, economics and interfaces between unit operations, and to provide a forum for discussions on case histories and operational difficulties. Topics covered include: leaching of metal values by chemical reagents or bacterial action at ambient or elevated pressures and temperatures; separation of solids from leach liquors; removal of impurities and recovery of metal values by precipitation, ion exchange, solvent extraction, gaseous reduction, cementation, electro-winning and electro-refining; pre-treatment of ores by roasting or chemical treatments such as halogenation or reduction; recycling of reagents and treatment of effluents.
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